WO2005115176A1 - Produit proteinique marin hydrolyse, son procede de production et son application - Google Patents

Produit proteinique marin hydrolyse, son procede de production et son application Download PDF

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Publication number
WO2005115176A1
WO2005115176A1 PCT/NO2005/000172 NO2005000172W WO2005115176A1 WO 2005115176 A1 WO2005115176 A1 WO 2005115176A1 NO 2005000172 W NO2005000172 W NO 2005000172W WO 2005115176 A1 WO2005115176 A1 WO 2005115176A1
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WIPO (PCT)
Prior art keywords
product
fish
protein
marine
stickwater
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PCT/NO2005/000172
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English (en)
Inventor
Eddy G. Torp
Osvald Torrissen
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Norcape Biotechnology As
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Priority to PL05747848T priority Critical patent/PL1765094T5/pl
Priority to US11/597,188 priority patent/US20080020097A1/en
Priority to DE602005008604T priority patent/DE602005008604D1/de
Priority to AU2005247277A priority patent/AU2005247277B2/en
Priority to ES05747848.9T priority patent/ES2311990T5/es
Priority to CA2568370A priority patent/CA2568370C/fr
Priority to EP05747848.9A priority patent/EP1765094B2/fr
Application filed by Norcape Biotechnology As filed Critical Norcape Biotechnology As
Priority to DK05747848.9T priority patent/DK1765094T4/en
Priority to CN2005800250538A priority patent/CN101001544B/zh
Priority to JP2007514960A priority patent/JP4807593B2/ja
Publication of WO2005115176A1 publication Critical patent/WO2005115176A1/fr
Priority to ZA2006/10349A priority patent/ZA200610349B/en
Priority to DKPA200601666A priority patent/DK177057B1/da
Priority to HK08100509.6A priority patent/HK1109838A1/xx
Priority to US13/712,238 priority patent/US20130156887A1/en

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Classifications

    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K20/00—Accessory food factors for animal feeding-stuffs
    • A23K20/10—Organic substances
    • A23K20/142—Amino acids; Derivatives thereof
    • A23K20/147—Polymeric derivatives, e.g. peptides or proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C9/00—Milk preparations; Milk powder or milk powder preparations
    • A23C9/14—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment
    • A23C9/142—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration
    • A23C9/1425—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration by ultrafiltration, microfiltration or diafiltration of whey, e.g. treatment of the UF permeate
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
    • A23J1/001—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from waste materials, e.g. kitchen waste
    • A23J1/002—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from waste materials, e.g. kitchen waste from animal waste materials
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
    • A23J1/04—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from fish or other sea animals
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J3/00—Working-up of proteins for foodstuffs
    • A23J3/30—Working-up of proteins for foodstuffs by hydrolysis
    • A23J3/32—Working-up of proteins for foodstuffs by hydrolysis using chemical agents
    • A23J3/34—Working-up of proteins for foodstuffs by hydrolysis using chemical agents using enzymes
    • A23J3/341—Working-up of proteins for foodstuffs by hydrolysis using chemical agents using enzymes of animal proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K10/00—Animal feeding-stuffs
    • A23K10/20—Animal feeding-stuffs from material of animal origin
    • A23K10/22—Animal feeding-stuffs from material of animal origin from fish
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K50/00—Feeding-stuffs specially adapted for particular animals
    • A23K50/10—Feeding-stuffs specially adapted for particular animals for ruminants
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K50/00—Feeding-stuffs specially adapted for particular animals
    • A23K50/30—Feeding-stuffs specially adapted for particular animals for swines
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K50/00—Feeding-stuffs specially adapted for particular animals
    • A23K50/40—Feeding-stuffs specially adapted for particular animals for carnivorous animals, e.g. cats or dogs
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K50/00—Feeding-stuffs specially adapted for particular animals
    • A23K50/60—Feeding-stuffs specially adapted for particular animals for weanlings
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C2210/00—Physical treatment of dairy products
    • A23C2210/20—Treatment using membranes, including sterile filtration
    • A23C2210/206—Membrane filtration of a permeate obtained by ultrafiltration, nanofiltration or microfiltration
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs

Definitions

  • Hydrolysed marine protein product process for the production thereof, and application.
  • the present invention relates to a hydrolysed marine protein product and a method for the production of said product. Further the invention relates to a feed product for animals, including humans, and a culture medium comprising the hydrolysed marine protein product.
  • the protein product may be hydrolysed by enzymatic activity, bacterial activity, acids, cooking or any combination of these.
  • the protein product may also include stickwater peptide fraction containing bioactive peptides.
  • Feed product could be any nutritional product comsumable by any animal including humans.
  • whey as animal feed is well established based on the functional properties of the proteins and the energy supplied by the lactose. Standard fishmeal is often added at approximately 5% to enhance performance. The feeding of young pigs with this is especially beneficial. Whey is also used for calf supplements, calf milk replacers and for dairy cows. In addition porcine and bovine plasma proteins have been used extensively as a feed to improve health, growth and general performance. The use of plasma proteins has now ended in the European Community following the recognition that feeding mammalian species with their own proteins can cause major health risks. The problems of BSE (Bovine Songiform Encephalopathy) are believed to have been caused by this practice.
  • BSE Bovine Songiform Encephalopathy
  • mammalian proteins unless from milk
  • animal feeds except carnivores
  • fish protein which is from a completely different genus which can be used to feed animals, including avaian, mammals and humans.
  • substitute proteins mainly soy flour
  • soy flour have been added to make whey substitutes.
  • These proteins are mainly in their raw, native state or as soy flour and there are problems associated with the digestion and absorption of these proteins.
  • Trypsin a natural proteolytic enzyme in the gut, is inhibited by certain amino acid sites present in soy proteins. This affects the digestibility for e.g. young pigs that have low levels of trypsin.
  • Fish proteins and fish meal have also been used historically as a good source of protein and minerals for the dairy, pig and poultry industries. They are naturally good sources of the essential amino acids lysine and methionine. Trace elements of iodine and selenium are also advantageous. This is set to continue and the demand will increase if the technical issues of purity, salt content and undesirable nitrogen compound levels are resolved.
  • the mixture of hydrolysed marine protein combined with the natural sweetness of lactose and the improved quality is all based on removing any unwanted biogenic amine by membrane technology as suggested here.
  • the symptoms of this after a short incubation period include a rash, facial flushing, vomiting, diarrhea, dyspnea (difficult or labored breathing), headaches and metallic/peppery mouth taste.
  • High levels of toxic amines are absorbed in the intestine, and normally de-toxified by the liver and then eliminated by the kidneys, but prolonged exposure ultimately provokes disorder in the organs cells, leading to liver and kidney failure.
  • According to the FDA in America fish with greater than 50 ppm histamine are considered spoiled, although poisoning generally occurs at greater than 200 ppm.
  • the use of spoiled fish, waste and the combination of poor handling generally leads to high levels of histamine in meal and other products.
  • Whey is the by-product of cheese and casein manufacturing. It has been used for centuries as a feed product for animals, especially dairy cows and pigs. It contains all the soluble milk proteins as albumins and immunoglobulins, and anti-microbial agents such as lactoferrin and lactoperoxidase. These are natures means of protection for young animals.
  • the development of membrane filtration has enabled dairy companies to exploit the value of these highly nutritious proteins for infant formula, bakery products, health foods and improved quality dairy products. In turn this has created a surplus of ultra filtration (UF) permeates that are often difficult to dispose of.
  • UF ultra filtration
  • the proteins constitute only 10-12% of the dry material in whey. The remaining 90% is made up of lactose and minerals, especially physiologically important macrominerals such as magnesium, calcium, phosphorus, and potassium, plus non-protein nitrogen.
  • the minerals present in UF permeate are utilized more effectively by the pig than the minerals in vegetable feeds. (Principles of Swine Nutrition - Texas A&M University).
  • Lactose forms approximately 75% of the remaining dry matter in whey and is the main energy source for infants in mammalian species. Efforts have been made to combine refined lactose produced commercially with synthetic amino acids to substitute whey in nursery diets (USA Animal and Dairy Science - Dove 1998) and shown that the performance is similar to whey. It has been demonstrated in these tests that lactose and amino acids can be substituted for whey in the diets of early weaned pigs for all but 5% of the whey in the diet. By reducing the whey in the diet pig producers can decrease the costs of the diets for early weaned pigs. In these tests a fish meal level of 5% was also present in all trials.
  • the challenge is to produce a high quality protein derivative from these by-products that has low mineral levels, especially sodium and chloride, and low levels of undesirable amine compounds and other rest products of enzymatic and microbial degradation of amino acids.
  • the current hydrolyzed protein products used e.g. as an ingredient in feed contains a high level of monovalent ions and biogenic amines which as described elsewhere are toxic and gives a bad taste to the product and is a problem.
  • a new hydrolyzed protein product comprising a significant reduction in the level of non protein nitrogen, amines and monovalent ions, reducing the toxic effect of biogenic amines and the high concentration of salt.
  • the present invention solves this problem by combining UF and NF thereby removing more than 70% of the water. The energy consuming evaporation step is thus almost eliminated.
  • An object of the present invention is to provide a hydrolyzed protein product or a purified stickwater with a minimum level of biogenic amines and monovalent ions from theNF.
  • Another object of the present invention is to provide a cost- effective process for the production of said product.
  • hydrolysate marine protein poduct comprising low salt, low biogenic amines and NPN ( non - protein nitrogen) is described.
  • This product is used as an ingredient of feed for animals, humans and microorganisms e.g. improving the quality of whole meal. Further it is utilized when blended with ultrafiltration permeate (75% lactose) from milk products as an improved animal feed ingredient, to substitute whey, milk, other protein substitutes such as soy, wheat and their derivatives, in feed formulas.
  • the present invention relates to a hydrolysed marine protein, a method for the production of said protein and the use of said protein in animal and human feed and culture media.
  • the invention relates to a hydrolysed marine protein product having a reduced level of monovalent ions and biogenic amine groups and other rest products of enzymatic, cooking, acids and microbial degradation or any combinaitn thereof.
  • the salt content arises from the salt content of the organisnm used and from the sea water used in pumping the fish.
  • the undesirable small nitrogen compounds are created by hydrolytic action on the protein source.
  • the process according to the invention comprises the following steps homogenizing by-product from fish and/or other marine industries/sources controlled hydrolyses of said proteins and/or separation of stickwater from processing of marine raw materials - utrafiltration to provide a clarified marine protein hydrolysate nanofiltration of the clarified UF permeate to remove monovalent ions and biogenic amines drying of the NF permeate and UF concentrate separately or a combination thereof by spray, vacuum drying or any other drying method.
  • the resultant purified concentrated blend of refined fish protein hydrolysate containing bioactive peptides can then be recombined with the oils and proteins when removed from the stickwater or alternatively blended with ultrafiltration permeates of whey or milk and milk products containing no significant levels of milk protein. This latter product can be used for animal feed.
  • a refined fish protein hydrolysate can also be prepared by enzymatic degradation of an acidified mix of fish processing by-products and processing by the same method.
  • these two products are combined to form a feed product with both the necessary protein and carbohydrate sources.
  • lactose in the ultrafiltration permeate of whey is especially beneficial as an energy source for young weaning pigs.
  • the addition of the fish protein hydrolysate treated by UF or stickwater UF permeate, supplies all of the essential, (particularly lysine) and non-essential amino acids. All the essential amino acids, trace elements and minerals are also present. Each has a specific role in supporting growth and nutrition, which is combined in this product.
  • the hydrolysed fish protein according to the invention can be widely used as a component of a variety of products.
  • the hydrolysed fish protein is intended as a feed product especially for porcine and bovine (dairy cow) species but it may be fed all types of animals, where fish diet is traditional (mink and fox for fur production) and is equally beneficial in animals such as domesticated feline and canine species as well as humans.
  • the invention substantially eliminates the problem of high levels of salts and biogenic amines and other rest products of enzymatic and microbial degradation of amino acids by the production of a higher quality product based on new methods of filtration.
  • the use of this process to produce an NF concentrate that is then combined with the milk sugars contained in milk protein permeate can help to improve flavor and mask any bitterness associated with peptones produced from hydrolysed proteins.
  • the protein hydrolysate contains high levels of sodium chloride. Bacterial degradation of protein creates histamine, and its derivatives, putrecine and cadaverine which are toxic.
  • the invention also relates to the significant removal of these undesirable compounds by using nanofiltration (NF) membranes on either the fish protein hydrolysate or stickwater permeates that have been treated by ultrafiltration. h doing so the UF permeate is concentrated by NF to a level of 4 to 5 times and the removal of up to 80% water containg a similar proportion of the undesirable solutes. This results also in significant energy savings of up to 50 % of the costs of standard evaporation.
  • NF nanofiltration
  • Another significant advantage of the hydrolysed marine protein product according to the invention and thus the feed product, is that the amount of monovalent ions is reduced compared to conventional animal feed. It is known that a high nutrition of monovalent ions (salt) leads to increased water consumption and a lack of sufficient water cause serious toxicity in animals, especially young ones. The toxicity symptoms are lack of diet, lack of balance, erratic behavior and ultimately death (lesions are typically found in the brain). The reduction of monovalent ions and lowering of the mineral content by use of the nanofiltration according to the invention improves the mineral profile. Nanofiltration therefore provides a protection of the young animals against such disorders and retains the important divalent compounds.
  • the use of nanofiltration on the clarified hydrolysate protein reveals in addition a significant reduction in the amount of amine groups, such as cadaverine, putracine, histamine and other unwanted amines that may be present as a result of microbiological degradation -often due to microorganisms which are normally present in the by-products as a result of poor handling, age, and not processing at source.
  • the common causative bacteria are Clostridium, Salmonella Proteus and Escherichia Coli and contamination occurs before the acidification of the silage.
  • the symptoms in fur animals of excessive histamine in the diet are diarrhea, decreased feed consumption, reduced body weight gain relative to feed intake in direct proportion to the level of Histidine found, vomiting and dilated stomachs. (Nutrient requirements of Mink and Foxes 1982 National Academy Press).
  • the invention uses techniques developed from the advances in the dairy processing industry where the large volumes (average of 1 million liters per day of liquid in a single factory) have led to cost reductions, efficient designs, better more resilient membrane technology and construction.
  • the membrane used is similar to that used in oil and water separation.
  • specific membrane materials are used that have been used in high salt content environments, that offer better resistance against fouling by fats and oils, that are significantly more hydrophobic and give better mechanical protection against low pH and the high temperatures of stickwater when used in these processes.
  • Better membrane selection and equipment design to optimize flow and pressure conditions allows for higher scale, more cost effective processing of marine protein hydrolysates or stickwater fractions containing bioactive peptides.
  • silage More traditionally the by-products from fish processing have been made into silage with he remains of the carcase after filleting, the viscera, and skeletons have all being used to make low grade fish meal from the silage. Whole fish such as capelin and herring are also used.
  • the standard process for silage is to collect the by-products and acidify with either mineral or organic acids to a pH below 4.0. This prevents bacterial growth and partially hydrolyses the proteins.
  • proteolytic enzymes that can operate at low pH further enhances the hydrolysis, producing a mixture of peptides, oils, slurry, bones and scales. This is sometimes homogenised to form an even mixture.
  • Centrifugal Separators are used to separate, the oils, and water.
  • the fish meal is produced from a blend of whole fish and/or silage that is cooked and sterilised. The resultant aqueous liquid by-products can be evaporated and the concentrates added back to the silage. These products often contain high levels of histamine and its derivatives that create off odours.
  • the hydrolysed protein provided by the method according to the invention may also be suitable for use in the pharmaceutical industry as a growth media.
  • the inventive process will enable producers to make enhanced feed.
  • Such feed will enhance performance in feeding (growth, energy, weight gain, health).
  • the new process will ensure that the level of l istamine and other biogenic amines are below the thresholds of spoilage.
  • the overall quality of whole meal and meal produced from silage will also be significantly increased.
  • an animal feed prepared by the combination of a clarified marine protein hydrolysate derived from either stickwater or silage, and blended with milk protein UF permeate is provided.
  • GMO gene-modified organisms
  • the aim of the invention is to provide new improved cost-effective healthy products with benefits for humans, animals and cultures - improve flavour of the hydrolysate by controlling the enzymic reaction produce an improved composition (more digestible protein with a higher nutritional value, better quality, less monovalent ions, less biogenic amine compounds) add value to the fish meal produced from whole fish and/or silage by improving overall quality when the components are recombined without the water and undesirable solutes reduce energy costs by concentrating the peptides while removing water and the undesirable solutes contained in the NF permeate a new ultrafiltration process, using high membrane density ceramic ultrafiltration membranes with an improved mechanical strength, at lower unit cost and production cost than previously obtained with hollow fiber, or tubular, or other ceramics and a significant advantage in temperature of operation above 50° C and up to 90° C with a pH range ltol4 a new nanofiltration, that selectively removes monovalent ions to improve the mineral balance, and removes unwanted NPN including biogenic amine compounds - a combination of these ultrafiltration and
  • FIG. 1 A schematic representation of the normal industry pathway and the new inventive pathway is shown in figure 1.
  • the level of monovalent ions, biogenic amines and other rest products are reduced by combining the steps of UF and NF, and the level are reduced to at least 40%> of the original. Additionally volatile organic soluble compounds are removed causing a reduced smell and an improve palatable product.
  • hydrolysed marine proteins may be obtained from any fish source to include, fish silage, fish by-products and stickwater from fish meal processing or from any aquatic species source to include, crab, shellfish, silage, by- products and stickwater and cooking water from processing or any combination thereof.
  • the invention relates to a method for the production of a hydrolysed marine protein product , comprising the following steps: homogenizing by-product from fish and/or other marine industries/sources controlled hydrolyses of said proteins and/or separation of stickwater from processing of marine raw materials utrafiltration to provide a clarified marine protein hydrolysate - nanofiltration of the clarified UF permeate to remove monovalent ions and biogenic amines drying of the NF permeate and UF concentrate separately or a mixture by spray, vacuum drying or any form of drying.
  • the ultrafiltration may preferentially be performed by high density ceramic membranes.
  • the nanofiltration may preferentially be performed by high selective membranes.
  • the steps of ultrafiltration and nanofiltration can operate on stickwater and cooking water at temperatures of greater than 60 C.
  • a further aspect of the invention is a feed product comprising the hydrolysed marine protein product and any carbohydrate source, vitamins, oils, fats and trace elements.
  • the feed is preferentially used where a balanced diet are needed for humans and animals especially young pigs, dairy cattle, mink, fox, domestic pets and other species.
  • This is accomplished by the present invention providing a feed of high quality containing beneficial fish protein, and reduced levels of monovalent ions and biogenic amines, and carbohydrate derived from any source, preferentially by-products of milk processing.
  • a further aspect of the invention is a micro-organism nutrition, wherin the hydrolysed marine protein product is used as a supplement for culture media.
  • a further aspect is that the UF and NF water removal process can exploit excess energy on ships hereby reducing cost and increasing the ships operation duration and radius.
  • Figure 1 is a flow chart showing how the production of hydrolysed marine protein product according to the invention differs from the normal industrial process.
  • Figure 2 is a curve showing the transmembrane pressure at a flow rate of 750 1pm
  • Figure 3 is a curve showing the transmembrane pressure at a flow rate of 850 1pm
  • Figure 4 is a curve showing the transmembrane pressure at a flow rate of 950 1pm
  • Figure 5 is a curve showing the transmembrane pressure at a flow rate of 1050 1pm
  • Figure 6 is a graph showing the UF permeation over time for different pressure of operation and feed solids.
  • Figure 7 is a graph showing the flux curve vs retentate concentration of stickwater at 80°C.
  • Figure 8 is a graph showing the reduction in flux rate against retentate volume concentration ratio (VCR).
  • Figure 9 is a graph showing the concentration using NF membranes of peptones, produced by enzymic hydrolysis of fish silage and ultrafiltration (permeate).
  • Figure 10 is a flow chart illustrating the removal of salts and biogenic amines by the combined UF and NF.
  • the starting material of the hydrolysed marine protein product according to the invention can be any marine protein source such as fish, by-products of fish, fish silage and stickwater from fish meal processing. To illustrate the process stickwater and silage is used.
  • Stickwater at 80° C contains oil, proteins, salts amines and water.
  • the first step is to remove oil by any suitable separation technique in the art. Following separation of the oil the UF is used to separate the proteins and remaining oils left after separation from the hydrolysed proteins amines and salts.
  • the retentate, i.e. the concentrated proteins and oils contain the gelatinous proteins that can then be returned to the meal to improve binding.
  • the permeate, i. e. the liquid that goes through the UF membrane which is the feed to the NF contains salt, amines and water. Some of the amines in the permeate are desirable, i. e. peptides and peptones. Others like the biogenic amines are not.
  • the content of biogenic amines is reduced by the NF membrane. These small molecular weight compounds pass through the membrane. The larger desirable amines are retained in the NF retentate. Salt removal is also beneficial in improving the product quality.
  • the NF allows the passage of water, very small amines and salts. The use of NF also concentrates these peptones because most of the water is lost as the salts etc are removed as permeate.
  • the UF retentate can be used as an enzyme product or added to meal.
  • FPC Fish Protein Concentrate
  • Part 1 - Determination of Operating conditions for the UF membrane The experiments were conducted using a SeparaTech CMF pilot plant with a Corning Ceramic element having a 0.01 micron pore size. When constructing a test protocol for ceramic membranes a series of initial tests are run at different cross flow velocities. This enables the experimenter to determine the most suitable flow rate across the membrane surface and the resultant pressure drop.
  • the Corning membrane was chosen for its unique monolithic structure. Unlike all other ceramic membrane systems, the membrane fills the vessel which gives a very uniform pressure change across the filter for different flow conditions. This enabled the selection of the optimum parameters for the separation of the proteins, oil and the peptones.
  • TMP transmembrane pressure
  • TMP Transmembrane pressures
  • the NF membrane was a PTI Company TFC (Thin Film Composite) spiral wound element with 1.14 m 2 of area.
  • the permeate flow rate was recorded and measurements taken of the retentate volume and dry matter. These values were used to calculate the volume concentration factor and the final dry matter achievable in the retentate. Permeate dry matter was also measured • by refractometer and samples taken to analyse the amount of salt removed and determine the losses of non protein nitrogen and salt. For the NPN (non-protein nitrogen) and protein a standard Kjedahl method was used to determine total nitrogen. The salt analysis was performed using a standard Silver Nitrate titration method.
  • HPLC HPLC which is the standard method for dete ⁇ nining the quality of fish meal and its classification in the fish industry.
  • the added advantage for the UF and NF processes is that the permeate is diluted and the retentate concentrated. The result of this is that over 70% of the water is removed (see Fig 10) prior to evaporation, saving substantial costs in energy. In some cases where the stickwater is highly gelatinous because of the type offish used, evaporation is eliminated, and a little more water is removed using the filter presses.
  • the volumetric concentration factor was 10 x so the mass balance shows a 90% removal of water containing 66.5% of the salt and 71.4% of the NH3/VN
  • the permeate also contained peptones and peptide fractions.
  • the total dissolved solids content of the permeate was 2.0%.
  • a typical feed strength to the UF when fish waste is hydrolysed is about 12 % TS and the resulting permeate is about 8% dry matter. Due to the hydroscopic nature of the peptones and the high osmotic pressure (the pressure needed to remove water) it is necessary to operate the NF at 30 bar and use diafiltration after a 50% removal of water top obtain the necessary concentration and removal of salt and amines.
  • the diafiltration ratio used was 1000 litres reduced to 500 and then 500 litres of water added to make up the volume to 1000 litres. The volume is then reduced as far as possible to get the required product with reduced salt and amines. The results obtained were in the region of an 8x concentration factor, with a resulting 87%o removal of salt and amines.
  • Table 6 NF concentration of UF permeate produced from silage hydrolysed by acid and proteolytic enzymes using a PTI TFC membrane with a surface area of 1.14 m 2 .
  • the results show that marine proteins that are hydrolysed by cooking, acid, enzymic action or a combination of any of these can be processed using UF and then NF to produce a reduced level of amine and reduced level of salt ( monovalent ions) compared to the levels achieved by conventional methods without UF and NF.
  • a temperature of a mimimum 50 °C and ideally 80 ° C must be used. At lower temperature the flux is too low due to the high viscosity of the proteins especially with some fish species.
  • the amines and monovalent ions are reduced to about 30% of the original mass in the feed stream. More than 70 % is removed.
  • the combined process results in a concentration of the oils and proteins (UF) and peptiones (NF) that reduces the use of energy in evaporation because water has aheady been removed. In some cases where concentration is high enough and the protein gelatinous enough, evaporation becomes unnecessary. This results in high energy savings.

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Zoology (AREA)
  • Animal Husbandry (AREA)
  • Birds (AREA)
  • Biochemistry (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Health & Medical Sciences (AREA)
  • Marine Sciences & Fisheries (AREA)
  • Molecular Biology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Nutrition Science (AREA)
  • Biomedical Technology (AREA)
  • Biotechnology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physiology (AREA)
  • Water Supply & Treatment (AREA)
  • Fodder In General (AREA)
  • Feed For Specific Animals (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Peptides Or Proteins (AREA)
  • Meat, Egg Or Seafood Products (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

La présente invention porte sur un produit protéinique marin hydrolysé et sur son procédé de production. L'invention porte également sur un produit alimentaire pour les animaux, ainsi que pour les hommes, et sur un milieu de culture comprenant le produit protéinique marin hydrolysé. Le produit protéinique peut être hydrolysé par une activité enzymatique, une activité bactérienne, des acides, la cuisson ou une combinaison quelconque de ces activités. Le produit protéinique peut également comprendre une fraction peptidique de liqueur visqueuse contenant des peptides bioactifs. Le produit alimentaire peut être un produit nutritif pouvant être consommé par tout animal, y compris les hommes.
PCT/NO2005/000172 2004-05-26 2005-05-24 Produit proteinique marin hydrolyse, son procede de production et son application WO2005115176A1 (fr)

Priority Applications (14)

Application Number Priority Date Filing Date Title
JP2007514960A JP4807593B2 (ja) 2004-05-26 2005-05-24 海洋タンパク質加水分解産物、その製造方法及び応用。
EP05747848.9A EP1765094B2 (fr) 2004-05-26 2005-05-24 Produit proteinique marin hydrolyse, son procede de production et son application
DE602005008604T DE602005008604D1 (de) 2004-05-26 2005-05-24 Hydrolysiertes meeresproteinprodukt, verfahren zu seiner herstellung und verwendung
AU2005247277A AU2005247277B2 (en) 2004-05-26 2005-05-24 Hydrolysed marine protein product, process for the production thereof, and application
DK05747848.9T DK1765094T4 (en) 2004-05-26 2005-05-24 Hydrolysed marine protein product, process for the preparation thereof and the use
CA2568370A CA2568370C (fr) 2004-05-26 2005-05-24 Produit proteinique marin hydrolyse, son procede de production et son application
US11/597,188 US20080020097A1 (en) 2004-05-26 2005-05-24 Hydrolysed Marine Protein Product, Process for the Production Thereof, and Application
PL05747848T PL1765094T5 (pl) 2004-05-26 2005-05-24 Produkt hydrolizy białka pochodzenia morskiego, sposób jego wytwarzania i zastosowanie
ES05747848.9T ES2311990T5 (es) 2004-05-26 2005-05-24 Producto de proteína marina hidrolizada, proceso para la producción del mismo, y aplicación
CN2005800250538A CN101001544B (zh) 2004-05-26 2005-05-24 水解的海洋蛋白制品及其制备方法和用途
ZA2006/10349A ZA200610349B (en) 2004-05-26 2006-12-11 Hydrolysed marine protein product,process for the production thereof,and application
DKPA200601666A DK177057B1 (da) 2004-05-26 2006-12-19 Produkt af hydrolyseret marint protein, fremgangsmåde til dets fremstilling og anvendelse
HK08100509.6A HK1109838A1 (en) 2004-05-26 2008-01-15 Hydrolysed marine protein product, process for the production thereof, and application
US13/712,238 US20130156887A1 (en) 2004-05-26 2012-12-12 Hydrolysed marine protein product, process for the production thereof, and application

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NO20042188A NO320964B1 (no) 2004-05-26 2004-05-26 Hydrolysert marint proteinprodukt og et fôrprodukt omfattende dette, fremgangsmate for fremstilling og anvendelse
NO20042188 2004-05-26

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EP (1) EP1765094B2 (fr)
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AT (1) ATE402618T1 (fr)
AU (1) AU2005247277B2 (fr)
CA (1) CA2568370C (fr)
DE (1) DE602005008604D1 (fr)
DK (2) DK1765094T4 (fr)
ES (1) ES2311990T5 (fr)
HK (1) HK1109838A1 (fr)
MA (1) MA28669B1 (fr)
NO (1) NO320964B1 (fr)
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ES2362067A1 (es) * 2009-12-15 2011-06-28 Jealsa Rianxeira, S.A. Procedimiento para la obtención de un extracto gelificable de proteínas a partir de agua de cocción de pescado.
WO2012078223A1 (fr) * 2010-12-06 2012-06-14 Framroze Bomi P Nouveau procédé pour produire un hydrolysat de protéine marine à contamination en métaux lourds ultra-faible
WO2014207497A1 (fr) * 2013-06-29 2014-12-31 Hofseth Biocare Asa Nouveau procédé de production d'hydrolysat de protéines d'origine marine à contamination ultra-faible en métaux lourds et des propriétés physiques améliorées
WO2019086657A1 (fr) * 2017-11-06 2019-05-09 Pg Flow Solutions As Navire de pêche doté d'une installation d'ensilage et procédé associé
EP3967151A1 (fr) 2020-07-14 2022-03-16 Goia Limited Valorisation de sous-produits d'animaux marins
EP3749339B1 (fr) 2018-01-30 2022-08-03 Aker Biomarine Antarctic As Hydrolysat de protéines marines ayant un faible taux de fluor et de triméthylamine
NO347050B1 (en) * 2021-09-01 2023-05-02 Kitin Antarktis As Stabilizing stickwater deriving from creatures living in a body of water
WO2023111607A1 (fr) 2021-12-15 2023-06-22 Goia Limited Valorisation de sous-produits issus d'animaux marins

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US8557297B2 (en) 2008-09-12 2013-10-15 Olympic Seafood, As Method for processing crustaceans and products thereof
JP6139056B2 (ja) 2008-09-12 2017-05-31 リムフロスト テクノロジーズ エーエス 蛋白質性濃縮物を生産する際にフッ化物含有量を削減するプロセス
US9814256B2 (en) 2009-09-14 2017-11-14 Rimfrost Technologies As Method for processing crustaceans to produce low fluoride/low trimethyl amine products thereof
US20100077654A1 (en) * 2008-09-23 2010-04-01 LiveFuels, Inc. Systems and methods for producing biofuels from algae
CL2009000292A1 (es) * 2009-02-09 2009-08-21 Ingenieria Ramfer Ltda Proceso de produccion de solucion concentrada al 50 % acidulada y polvo seco de peptidos, a partir de productos y residuos proteicos de origen animal pesca y acuacultura.
WO2010104908A1 (fr) * 2009-03-11 2010-09-16 LiveFuels, Inc. Systèmes et procédés de régulation de la biomasse algacée
WO2010121094A1 (fr) 2009-04-17 2010-10-21 Livefuels. Inc. Systèmes et procédés pour cultiver des algues avec des bivalves
KR101160325B1 (ko) * 2009-12-21 2012-06-28 전라남도 키조개 소스의 제조 방법
UA111078C2 (uk) * 2011-05-03 2016-03-25 Нестек С.А. Гідролізат білкового субстрату і спосіб його виготовлення
US9487716B2 (en) 2011-05-06 2016-11-08 LiveFuels, Inc. Sourcing phosphorus and other nutrients from the ocean via ocean thermal energy conversion systems
CN103355501A (zh) * 2013-08-01 2013-10-23 青岛和美饲料有限公司 一种添加生物活性肽的生长肥育猪饲料和制备方法
WO2016009364A1 (fr) * 2014-07-14 2016-01-21 Scotland Rebecca Isolement d'oligopeptides végétaux et leurs utilisations
WO2017030452A1 (fr) * 2015-08-17 2017-02-23 Ribaudo Bernales Fernando Ricardo Méthode pour l'élimination du sel de l'eau de colle de poisson par électrodialyse
EP3081094B1 (fr) * 2015-08-17 2018-11-07 Ribaudo Bernales, Fernando Ricardo Procédé d'obtention d'un aliment déshydraté à teneur élevée en protéines hydrolysées à partir d'eau de colle de poisson
KR101721972B1 (ko) * 2016-07-20 2017-03-31 한석운 알카라인 반응 및 인지질 수소화를 이용한 오징어 및 생선 부산물로부터 단백질 농축 분말사료 제조 방법
BR112019023384A2 (pt) * 2017-05-18 2020-06-16 Firmenich S.A. Composições de hidrolisado de proteína marinha com mau odor reduzido
EP3799721A1 (fr) * 2019-10-02 2021-04-07 Mars Incorporated Procédés de traitement de protéines animales

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2362067A1 (es) * 2009-12-15 2011-06-28 Jealsa Rianxeira, S.A. Procedimiento para la obtención de un extracto gelificable de proteínas a partir de agua de cocción de pescado.
WO2012078223A1 (fr) * 2010-12-06 2012-06-14 Framroze Bomi P Nouveau procédé pour produire un hydrolysat de protéine marine à contamination en métaux lourds ultra-faible
WO2014207497A1 (fr) * 2013-06-29 2014-12-31 Hofseth Biocare Asa Nouveau procédé de production d'hydrolysat de protéines d'origine marine à contamination ultra-faible en métaux lourds et des propriétés physiques améliorées
WO2019086657A1 (fr) * 2017-11-06 2019-05-09 Pg Flow Solutions As Navire de pêche doté d'une installation d'ensilage et procédé associé
EP3749339B1 (fr) 2018-01-30 2022-08-03 Aker Biomarine Antarctic As Hydrolysat de protéines marines ayant un faible taux de fluor et de triméthylamine
EP3967151A1 (fr) 2020-07-14 2022-03-16 Goia Limited Valorisation de sous-produits d'animaux marins
NO347050B1 (en) * 2021-09-01 2023-05-02 Kitin Antarktis As Stabilizing stickwater deriving from creatures living in a body of water
WO2023111607A1 (fr) 2021-12-15 2023-06-22 Goia Limited Valorisation de sous-produits issus d'animaux marins

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CA2568370A1 (fr) 2005-12-08
EP1765094A1 (fr) 2007-03-28
DK1765094T3 (da) 2008-12-01
PT1765094E (pt) 2008-11-03
DE602005008604D1 (de) 2008-09-11
NO20042188D0 (no) 2004-05-26
CA2568370C (fr) 2013-10-29
AU2005247277B2 (en) 2010-05-20
JP2008500040A (ja) 2008-01-10
ES2311990T5 (es) 2015-11-13
ES2311990T3 (es) 2009-02-16
EP1765094B2 (fr) 2015-08-26
DK177057B1 (da) 2011-04-11
NO20042188L (no) 2005-11-28
ATE402618T1 (de) 2008-08-15
AU2005247277A1 (en) 2005-12-08
CN101001544B (zh) 2010-11-17
PL1765094T3 (pl) 2009-01-30
HK1109838A1 (en) 2008-06-27
NO320964B1 (no) 2006-02-20
PL1765094T5 (pl) 2016-02-29
US20130156887A1 (en) 2013-06-20
MA28669B1 (fr) 2007-06-01
JP4807593B2 (ja) 2011-11-02
US20080020097A1 (en) 2008-01-24
DK200601666A (da) 2007-02-26
EP1765094B1 (fr) 2008-07-30
DK1765094T4 (en) 2015-11-09
CN101001544A (zh) 2007-07-18
ZA200610349B (en) 2008-04-30

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